2017
DOI: 10.3390/ma10040430
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Effect of Elemental Sulfur and Sulfide on the Corrosion Behavior of Cr-Mo Low Alloy Steel for Tubing and Tubular Components in Oil and Gas Industry

Abstract: The chemical degradation of alloy components in sulfur-containing environments is a major concern in oil and gas production. This paper discusses the effect of elemental sulfur and its simplest anion, sulfide, on the corrosion of Cr-Mo alloy steel at pH 2 and 5 during 10, 20 and 30 h immersion in two different solutions. 4130 Cr-Mo alloy steel is widely used as tubing and tubular components in sour services. According to the previous research in aqueous conditions, contact of solid sulfur with alloy steel can … Show more

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Cited by 23 publications
(11 citation statements)
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“…Since steel plays a crucial role in petroleum industry, companies have prioritized finding ways of protecting steel rather than replacing it by other materials. Some of the ways consist of alloys, coatings, special treatments or inhibitors [ 10 , 11 , 12 , 13 , 14 , 15 , 16 , 17 ], in which the inhibitors have been demonstrated possessing the most suitable advantages. Most of today’s commercial corrosion inhibitors are amine-based as well as its derivatives.…”
Section: Introductionmentioning
confidence: 99%
“…Since steel plays a crucial role in petroleum industry, companies have prioritized finding ways of protecting steel rather than replacing it by other materials. Some of the ways consist of alloys, coatings, special treatments or inhibitors [ 10 , 11 , 12 , 13 , 14 , 15 , 16 , 17 ], in which the inhibitors have been demonstrated possessing the most suitable advantages. Most of today’s commercial corrosion inhibitors are amine-based as well as its derivatives.…”
Section: Introductionmentioning
confidence: 99%
“…A quantitative analytical method was used to calculate the corrosion rate of each specimen based on the predicted weight change of low-carbon steel. The corrosion rate of specimen can be calculated using the equation [ 27 ] of: where C r is the corrosion rate of the low-carbon steel specimen (in mm/y), W L is the weight change of the low-carbon steel specimen (in mg) and t is the immersion time (in h), is the density of the low-carbon steel specimen (in g/cm 3 ).…”
Section: Methodsmentioning
confidence: 99%
“…A quantitative analytical method was used to calculate the corrosion rate of each specimen based on the predicted weight change of low-carbon steel. The corrosion rate of specimen can be calculated using the equation [27] of:…”
Section: Determination Of the Weight Change And Corrosion Ratementioning
confidence: 99%
“…Sulfur species are among the most undesirable constituents in crude oil since they decrease the quality of the products. In addition, they can cause catalyst poisoning and corrosion of the processing equipment as well as various problems related to product odor and storage stability. Sulfur can have an effect in crude oil fouling, with thiols, sulfides, and some condensed thiophenes to be considered as the most problematic . Free sulfur, disulfides, and thiophenol have been found to promote sludge formation, while the presence of hydrogen sulfide is extremely corrosive at high temperatures. , A major problem in the refinery heat exchangers is the formation of corrosion fouling due to chemical reactions triggered by sulfur compounds in crude oil on metallic surfaces.…”
Section: Introductionmentioning
confidence: 99%